GB2201961A

GB2201961A - Process for the preparation of rigid polyurethane

Info

Publication number: GB2201961A
Application number: GB08805114A
Authority: GB
Inventors: Sodario Olzewski Souto; Wilson Goncalves De Moura
Original assignee: Brastemp SA
Current assignee: Brastemp SA
Priority date: 1987-03-11
Filing date: 1988-03-03
Publication date: 1988-09-14
Anticipated expiration: 2008-03-03
Also published as: NO881075L; SE8800820L; MX167919B; FR2612192A1; CS273342B2; JPH02138328A; LU87157A1; GB8805114D0; DK130288D0; GB2201961B; YU45491B; IT8819654A0; NO881075D0; SE8800820D0; GR880100146A; AR243209A1; DE3808164A1; YU48888A; NL8800563A; BE1001674A5

Description

1 RIGID POLYURETHANE PREPARATION PROCESS ZiO 19 6 1 The present invention

relates to a process for the preparation of rigid polyurethane, reinforced or not# appropri- ate to replace sheets and other steel parts in home appliances such as refrigerators# freezers. laundering machines# dishwashers, clothes driers and microwave ovens. The methods currently known for the manufacture of home appliances of the so-called white line present some draw- backs related to the use of steel panels and other structural parts. In- these conventional techniques. the use of steel parts. particularly plates# limitates the shape variations of the assembly. requires various manufacture operations to reach the final preparation.for assembly of the home appliance and the use of internal filling of the panels with an insulating material in the cases of refrig erators and freezers, and requires special treatments to minimize the effects of coirosion, which is never entirely eliminated. % In view of the drawbacks of the state of the art for the manufacture of those home appliances, the development of a new product in polyurethane was proceeded with for the construction of panels and other parts of those devices. The replacement of metallic parts by polyurethane parts

in automotive vehicle components such as bumpers and other industrial fields is already well-known. However, many of the known polyurethane products that replace metallic parts assume for form of elastomers having an elongation greater.than 100%,, considering the ASTM D-638 standard of

1977 for the elongation test method. Alsoi these polyurethane composites obtained from the basic chemical reaction between a composition containing hydroxyl groups (polyols) and a composition possessing NCO radicals (aronatic poly-isocyanates)' in the presence of catalysts and other property-adjusting additives# display elastomeric characteristics that render them inappropriate for the t replacement of rigid metallic elements of the above defined white-line home appliances. Examples of these elastomeric polyurethanes employed in. the so-called RIM (Reaction Injection Molding) processes can 5- be found on US patents 4#243p760,, US 4,444,910 and US 4.540.768 which describe the reaction of a polyol (polyether, aminated polyester or polymer) having a high molecular weight. a poly-isocyanate (aromatic or otherwise) and a chain extender (aromatic diamine or amine-terminated).

Other currently known polyurethane products assume the form of rigid, nonelastomeric polyurethanes also resulting basically from the reaction of a polyol with a poly-isocyanate in the presence of catalysts, chain extenders and other additives. Even though they are arigid product.these polyurethanes are non-cellular, leading to the obtention of products having a high and undesirable hardness and a low thermal insulation capacityr which render them unsuitable for the construction of panels for said home appliances and also. in terms of thermal insulation characteristicsi they are defficient in the construction of panels for refrigerators and freezers. The document BR 188,162/67 describes certain polyurethane material of the above mentioned type that includes the addition of a small quantity of uncured epoxy resin to a composition containing polyurethane resin,, in order to increase the resistance to deformation by heat and color stability of the rigid, non- elastomeric and non-cellular polyurethane products. Still other known polyurethane products are prepared by 30the reaction of three polyols with poly-isocyanatess, and a polyurethane of this type is described on the patent document-BR 79042520 having a ratio of bending modulus -29 0 C/700C no higher than -3.4 and with one of the three polyols having a reactivity towards the poly-isocyanate 35higher than the reactivity of either of the two other polyols (active hydrogen compositions). Also in this case, the polyurethane products obtained have characteristics that render them unsuitable for the replacement of plate panels in white-line home appliances# as they necessarily employ three polyols and have a ratio of flexural modulus which notwisthstanding its being within the range of the present invention, is related to very low test values to allow the utilization thereof in home appliances. The present invention relates to a process for the preparation of a rigid# thermo-stable. cellular or micro;;;-cellu- lar polyurethane. reinforced or otherwiser with an elongation lower than 100%, preferably between 2 and. 50%1,. havi.ng a density ranging between 0.20 to 1.30-g/cm 3,, preferably about 0.60 g/cm3, the rigid polyurethane product beingobtained by the mixing and reaction of: a.resin defined by at least one polyether polyol and/or a polyester polyol selected among the aminated and non-aminated onesi derived from sucrose and propylene oxid. having a molecular weight ranging from 100 to 5,000. hydroxil numbers between 30 and 500 and viscosity-from 10D to 10.000 centipoise and in a quantity of 5 to 100 parts by weight of resin,.; and an aromatic poly- isocyanate selected from the group defined by toluene diisocyanate (TDI) and diphenylmethane diisocyanate (MDI) having a viscosity from.8 to 1000 centipoise, with a NCO percentage of 30 to 40 an& in quantit ' ies from 90 to 150 parts by weightr the mixture ratio between the two isocyanate (NCO) and resin (OH) NCO/OH components ranging from 0.60 to 2.20. The invention also relates to the product obtained by the above-mentioned reaction.

In addition to the basic compositions mentioned above (polyols and polyisocyanates)i the product-in question may includet as reaction components# cell-size adjusting agents# chain extension agents# expansion agents# reinforcement agents and flame-retarding agents.

The rigid polyurethane product obtained from the reactions mentioned above is particularly useful for the replacement 4.

of steel sheets in home appliances, particularly those of the so-called white-line. as they present the following advantages: - the polyurethane composition can be injected and acquires the shape of the mold, thereby providing a greater design versatility; it possesses a quick processing cycley thereby increasing productivity; it is an insulating material being recommended for systems requiring energy and food conservation, such as refrigerators and freezers.. it is a corrosion-resistant material# thereby solving the problems of replacing partsworn by oxidation or corrosion caused by chemical products; - it is amenable to painting by conventional processes# facilitating the utilization thereof for aesthetic pur- poses; it allows decorative applications in the most varied shapes and processes, such as hot-stamping adhesivest silk-screen# etc.; it possesses mechanical strength at low and high temper atures.

The composition for obtention of the rigid polyurethane polymer having physical-chemical properties suitable for the replacement of steel in home appliances is directly related to the selection of the raw materials and the amount thereof employed. The raw material employed in the production of the resin basically includes:

a) A mixture of polyether polyols and polyesthers - aminated or noto derived from sucrose and prolylene oxidei having a molecular weight ranging from 100 to 3000. hydroxyl number from 30 to 450 and a viscosity in centipoise of 100 to 10.000; the amount employed ranges from 5 to 100 parts by weight of the resin. The polyether polyols are prepared by the reaction of an alkylene oxide and those derived there- 1 i from, with compositions containing active hydrogen as promoter. The most widely employed alkylene oxides are# for example,, the ethylene oxide and the propylene oxide. The promoters of choice include ethylene glycol, propylene ' glycol# butanodiol,, glicerint trimethylolpropanet pentaerythritol. sorbitol, sucrose and mixtures thereof. Other promoters for aminated polyols are: ammonia. ethylenediaminet-diethylenotriamine,, toluenodiamine, diamino-diphenylmethane. triethylenotetraminer ethanolamine and mixtures thereof. As an example of processes for the obtention of polyether polyols we can mention - American patents Nr. 2, 948;757 and 3.000.963. Polyester polyols result from the reaction of a carboxyl- lic'acid or anhydride with a polyhydric alcohol. The most common acids are the adipic acid. phtallic acid# and phtallic anhydride; the alcohols are ethylene glycol# propylene glycol, dipropylene glycol. trimethylpropaner mannitol. sucrose and mixtures thereof. In addition to the above mentioned mixture# the resin may also contain: b) an agent to adjust the size of cells formed, also known as agent responsible for the breaking of surface tension or surfactant agent, which is a silicone derived from polydimethylsiloxane. employed as 0.1 to 5 parts by weight of the resin-," The American patent Nr. 3,,194,,773 describes agents of this type. c) a chain extender agent which can be a diol. triol or amines, such as glicerint diethylene glycolo 1-4 butanediolp ethylene glyco 1,, propylene glycol. diethylene diaminei 2j,4 diaminotoluene. 1,3 phenylenediaminei 1-4 phenylene diamine and mixtures thereof, employed in 0 to 30 parts by weight of the resin. d) As expansion agentsi responsible for the growth and -low-thermal conductivity coefficient (k-factor) of the polymer formedr which is a trichloromonofluoromethane used as 0 to 50 parts by weight of the resin.

e) A catalyst based on tertiary ammines and/or tin, responsible for the directing and speed of the reaction and the curing time,,- which are: 113 diaminopropane,, ethanolamine,, diethylenodiamine, tetramethylenodiamine, diaminocyclohdxane, hexamethylenodiamine, triethylenotetramine,, dimethylcycloh exylaminer tetraethylenopentamine, tin octotate, tin oleate, tin dibutyldilaurate, tin dibutyldioctoate and mixtures thereof, employed as 0.1 to 8 parts by weight of the resin. f) A reinforcing agent# which is responsible for the struc- tural part of the polymer formed: milled or hammered glass fiber is ehiployed, as well as r:rde husks, coffee husks#, corn husks and polypropylene strands, mineral charges such as calcium carbonate, talce mica, glass micro spfieresf etc., employed from 0 to 50 parts by weight of the resin... g) A flame retarding agent, which is the diethyl N#N (2- - hydroxyethyl)aminoethylphosphate and tri(B-chloro-isoprop-I) phosphate, employed from 5 to 30 parts by weightof theresin. The resin formed from the above defined elements is mixed in a stoichiometric manner with an aromatic poly-isocyanate responsible for providing the NCO groups whiche by reacting with the other componentsp forms the polyurethane. The most employed raw materials are the toluene-diisocyanate (TDI)t the diphenylmethane-diisocyanate (MDI) and a pre polymer of TDI or MDI, having a viscosity.ranging from 8 to 1,000 and a NCO percentage of 30 to 40, employed from 90 to 150 parts by weight. There are various methods for the preparationof isocyanatesp but.the commercially employed one is the phosgenation of primary amines. The main route for obtention of the TDI is from toluene which, through nitration, allows the obtention of a mixture of mononitrotoluene isomers; after a new nitration-, the 2,4 dinitrotoluene (80%) and the 2.6 dinitrotoluene (20%) are obtained; after a reduction and phosgenation, one arrives at the toluene diisocyanate 80/20, a mixture of isomers which is commercially called TDI.

z f 1 X The route for obtention of MD1 is from aniline and formaldehyde; after a condensation and subsequent phosgenations one obtains the diphenylmethane 4,4 diisocyanatel commercially known as MDI. The mixture of raw materials from item a" up to item "g" in defined proportions is giventhe name of resin.. The rigid polyurethane composition is the result of the chemical reaction between the resin and the isocYanater this being performed by an appropriate injection machine# that makes the mixture of the two components. The process for obtention of rigid polyurethane parts-and panels,, reinforced or not. having a density ranging from 0.20 to 1.30 g/em 3, is done by ijecting this mixture in an appropriate mold able to resist thegrowth pressure.

In a few seconds the mixture acquires the mold shape and in 1 to 10 minutes the part is finished and can be removed from the mold. As with other polymeric materialt the properties of polyurethane polymers are related to the molecular weighti the inter-TOlecular.forcest the stiffness# segments of the polymer chain. crystallinity and the degree of cross linkings. The strength tests have shown that. by increasing the items mentioned abover there is a non directly proportional increase in the properties of the polyurethane polymers.. In the case of the instant invention this Is exactly what happens; the selection of the raw material responsible for these items is fundamental to obtain a product having the properties of thermal insulation. resistance to impacts, mechanical strength and corrosion resistance to replace steel in home appliances.

We describe below some examples of the compositions of raw material and the properties thereof, which should not be deemed as limiting the invention. EXAMPLE 1 - In the preparation of the resin,, the'following.raw materials, were mixed:- 40 parts by weight of a polyether polyol M 450 and hydroxyl number 410. 5 parts by weight of a polyether polyol MW 1j000 and hydroxyl number llof 30 parts by weight of a polyether polyol MW 4. 700 and hydroxyl number 34# 60 parts of a polyester polyol MW 280 and hydroxyl number-430: 2 parts by weight of a surfactant derived from dimethylpolysiloxane MW 5.000 and hydroxyl number 115. 2.5 parts by weight of an amine catalyst dimethylcyclohexylaminer 20 parts by weight of trichloromonofluoromethane. This mixture was mixed with 98.8 parts by weight of toluene diisocyanate in an appropriate blender at a controlled speed. the mixture being' i- njbcted in a rectangular-shape mold. After curing# samples were extracted to perform'the Tests listed on Table 2.

EXAMPLE 2

In the preparation of the resin, 50 parts by weight of a polyether polyol MW 450 and hydroxyl number 410; 50 parts by weight of an aminated polyether polyol MW 480 and hydroxyl number 470; 2.5 parts by weight of a dimethylpolysiloxane surfactant, M11 SyOOO; 2 parts by weight of tetramethylenediamine catalyst and 10 parts by weight of trichloromonofluoromethane were mixed. This resin was mixed with 110 parts by weight of diphenylmethane diisocyanate in an appropriate blender at a controlled speedl the mixture being then injected in a rectangular- shaped mold.

Test samples were removed af ter curing, to perform the tests listed on Table 2.

EXAMPLE 3

For preparation of the resint 80 parts by weight of a polyether polyol MW 450 and hydroxyl number 410; 20 parts by weight of a pblyesthdr- polyol MW 280 and hydroxyl number 430; 2.5 parts by weight of dimethylsiloxane MW 5t000 dissolved in dipropyleneglycol with hydroxyl number 115# 3.0 parts by weight of tetramethylethylenediamine and 10 parts by weight of trichloromonofluoromethane were mixed.

This resin was mixed with 120 parts by weight of diphenyl- i, methane diisocyanete in an appropriate blender at a controlled speed, the mixture being injected in a rectangular-shape mold. Samples were extracted after curing, to perform the tests listed on Table 2.

EXAMPLE 4

For preparation of the resin, 80 parts by weight of a poly. ether polyol MW 450 and hydroxyl number 410; 20 pafts by weight of a polyesther polyol MW 280 and hydroxyl number 430; 3.0 parts by weight of dimethylpolysiloxane; 3.0 parts by weight of tetramethylethylenediamine; 10 parts of trichloromonofluoromethane and 5 parts by weight of 3.1 mm long milled fiberglass were mixed This resin was mixed with 120 parts by weight of toluene diisocyanate in an appropriate blender at a controlled speed,, the mixture being injected in a rectangu lar- shaped mold. Samples were taken after curing to perform the tests listed on Table 2.

Characteristics of the Raw Material Product Polyol I.....................

Polyol II 000.000000 Polyol-III 0000.000000 Polyol IV 0 0 Polyol V o.................... Dimethylpolysiloxane oeoeeoo Tetramethylethylenediamine Dimethyldichlorohexylamine 30 Trichloromonofluoromethane, Toluene diisocyanate Diphenylmethane diisocyanate 1 viscosity cp 8,'000 175 l;000 58,000 10,000 434 410 110 34 470 430 115 --- 120-800 OH Nr. Miq 450 1,,000 4,300 480 280 5#000 116 127 137,4 182,2 242 1.

1 t_ X % NCO Products Density Refr. Index g/cm 3 Polyol I Polyol II Polyol III Polvol I 1.080 1.008 1.018 1.110 1.236 1.052 0.770 0.850 0 0 6.. 0. 0 0 0 0 0 0 0 0 0 0 0 a Polyol V........... Dimethylpolysiloxane 10 Tetramethylethylenediamine Dimethylcyclohexylamine oo4iooo Trichloromonofluoromethane....

Toluene diisocyanate 1.25 DiphenyImethane diisocyanate 1.23 1.467 1.451 1JS6 1.478 1.587 1.454 ----- Note: The Polyols It JIt III are polyethers derived from sucrose and propylene oxide The Polyol IV is an aminated polyether derived from sucrose and propylene oxide polymerized with a tertiary amine. The Polyol V is a polyester. derived from the residue of 20 dimethyltherephtalate and dipropyleneglycol.

TABLE 2 (Properties) I t e m E x a m p 1 e s 1 2 3 4 Density, g/cm 3 0.40 -0.60 0.60 0.60 Cream timer sec. 13 18 16 19 Gel timer. sec. 36 40 33 33 Take free# sec. 60.55 49 65 Stirring time, sec. 4 6 6 10 Mold temperaturet 0 C 25 25 25 25 cont., & 1 1 1 i 1 - 11 I t e m Demolding; min.

Heat sag at 500c, mm Heat sag at 700c,, mm Tensile strength, MPa Elongation, % Flexural srength, mPa K.Factor - (W(M.K.) Water absorption, Shore A hardness Rockwell R hardness Corrosion resistance Impact resistance.Izod j/m 0.3 non-corroding.

E X a m p 1 e s 1 2 3 19 30 12 3 -0.7 0.048. 4 80 110 THE POLYOL EFFECT 2 10 20 3 36.5 0.038 M 100 100 3 5 is 10 32.8 0.041 1.4 100 63 1.5 2 21 4 37.5 0.042 3 100 53 13.7 20.8 21.4 The reaction of the hydroxyl groups of polyols with isoCyanate is a typical example of formation of polyurethane; the different hydroxyl numbers and molecular weights provide different properties to the group formed. In the case of rigid polymers# as in this Inventiont the graphs illustrated on figures li 20 4g 5 of the drawings appended show an improvement in the strength-of the product by decreasing the high molecular weight polyols, and increasing the low molecular weight polyols. In general# the low molecular weight and high hydroxyl number polyols are used for cellular or micro-cellular rigid polymers# whereashigh molecular weight and lower hydroxyl number polyols are used for flexible polymers and elastomersi etc. The combination of these polymers provides intermediate properties to the polymer formed.

THE SURFACTANT EFFECT The surfactant or cell stabilizer is a wet agenti responsible for the uniform size of the cells formed. A low surfactant level provides larger non-uniform cellsi whereas 5 an appropriate level produces small and uniform cells. In the case of the propertiesi the effect is dilluted due to the influence of the other compositions buti microscopically, this effect can be observed and measured. that is. the cell size can range from 2 to 200 microns.

THE CATALYST EFFECT As shown on figura 7, an increase in the catalyst level decreases the cream. gel and free adhesion time when we consider similar systems. as in systems having various polyols this occurs but not in a proportional manner. The amine and tin-based catalysts serve to direct the reaction between the isocyanate and the hydroxyl compounds in a quick manner to prevent cell collapse and so that the polymer can cure in.a pre-established manner.

THE BLOWING AGENT EFFECT The most employed agent for rigid polymers is the trichlorO- monofluoromethane M-11) which. due to its properties and encapsulation thereof in the cells, provides much improved. insulating properties (low K factor) to the polymer. in addition to being a physical agent that. decreases the resin viscosityp facilitating the processing. The decrease of R-11 concentration increases the polymer's density,improves the mechani:al properties (see figures 10 2r 4). The thermal insulationts a function not only of the amount of R-11. but also of the other raw material and the effect thereof is not directly proportional to R-11 (see figure 5).

11 - -1, THE ISOCYANATE EFFECT The reaction of isocyanate compounds with hydroxyl containing compounds produces the urethane polymeri in the case. of rigid polyurethanes. the selection of raw materials should be directed towards the -formation of crosslinks that.provide mechanical strength to the polymer formed. In the examples cited we can.observe that the best properties are obtained in those employing MDI; -this is explained by the fact that it has a molecule more appropriate for the formation of 10 crosslinks than the TDI.

THE FILLERS EFFECT The function of the fillers is increasing the filling and provide a better mechanical strength to the polymer (see figures 11 2, 3 and 4); we can mention example 4j which had its mechanical properties considerably- improved with the introduction of fiberglass. Based on the effects of each raw material on the final polymer and the their respective properties, we can relate each example and its respective application; the examples of 1 to 3 are employed in the manufacture of panels and parts for refrigerators and freezers# due to their insulating properties and corrosion-resistance; example 4'is employed in the manufacture of panels and parts for laundering machines, dish-washerst clothes driers and microwave ovens, due to their tensile strength, structural effect# impact resistance and total absence of corrosion.

Claims

1. PROCESS FOR THE PREPARATION OF RIGID POLYURETHANE, thermally stablei cellular or micro-cellular. reinforced or pot# with elongation lower than 100%# preferably between 2 and 50% and having a density ranging from 0.20 to 1.30 g/cm 3 p preferably around 0.60 g/cm 3, characterized in that it Includes the stage of reacting a resint defined by at least one polyether polyol and/or a polyester polyol selected among the aminated and non aminated ones, derived from sucrose and propylene_oxide. with a molecular weight og 100 to 5.000. hydroxyl number between 30 and 500 and a viscosity of 100 to 101000 centipoise and in-an amount of. 5 to 100 parts by weight of resin# with an aromatic polyisocyanate selected from the group defined by toluene diiso- cyanate (TDI) and the diphenylmethane diisocyanate (MI) having a viscosity of 8 to 1000 centipoiser with a NCO percentage of 30 to 40 and in an amount of 90 to 150 parts by weight of resin. 2. PROCESS FOR THE PREPARATION OF RIGID POLYURETHANE, in accordance with claim 1, characterized in that the resin includes from 5 to 100 parts by weight of an aminated polyether polyol. 3. PROCESS FOR THE PREPARATION OF RIGID POLYURETHANE,, in accordance with claim 1. characterized in that the resin includes from 5 to 50 parts by weight of a polyester polyol derived from residues of dimethylterephtalate and dipropyleneglycol. 4. PROCESS FOR THE PREPARATION OF RIGID POLYURETHANE, in accordance with claim 1. characterized in that the resin includes from 0. 1 to 5 parts by weight of a cell size adjusting surfactant agent. defined by a silicone derived from a polydimethylsiloxane. 5. PROCESS FOR THE PREPARATION OF RIGID POLYURETHANE, in accordance with claim 1, characterized in that the resin includes ' from 0 to 30 parts by weight of a chain extender agent selected between a diol and a triol.

4 6. PROCESS FOR THE PREPARATION OF RIGID POLYURETHANE# in accordance with claim 5, characterized in that the extender agent Is selected from the group comprised of glicerin. di- ethyleneglycol and 1-4 butanediol.

7. PROCESS FOR THE PREPARATION OF RIGID POLYURETHANEp in accordance with claim lr characterized in that the resin includes from 0 to 30 parts by weight of an expansion agent comprised of trichloromonofluoromethane.

8. PROCESS FOR THE PREPARATION OF RIGID POLYURETHANE,, in 10 accordance with claim 1,, characterized in that the resin includes from 0A to-8 parts by weight of a catalyst based on tertiary amines and/or tin. defined by one among tetramethylethylenediamine and dimethylcyclohexylamine. tin dibutyldilaurate and tin octoate.

9. PROCESS FOR THE PREPARATION OF RIGID POLYURETHANE# in accordance with claim 1. characterized in that the resin includes from 0 to 50 parts by weight of a reinforcing agent selected from the group consisting of milled or hammered fiberglass roving; rice husks, corn husks, coffee husks# polypropylene and polyethylene_strands and mineral charges.

10. PROCESS FOR THE PREPARATION OF RIGID POLYURETHANE, in accordance with claim 10 characterized in that the resin includes from 5 to 30 parts by weight of a flame retarding agent defined by diethyl N.N-bis (2-hydroxyethyl) aminoethylphosphonate of tri-(B-chloroisopropyl) phosphate. 11. Process for the preparation of a rigid polyurethane substantially as hereinbefore specifically described with particular reference to the Exaffples.

12. Rigid polyurethane when produced by a process as clain-ed in any one of claims 1 to 11.

Published 1988 at The Patent Office, State House, 66/71 High Holborn, London WClR 4TP. Further copies may be obtained from The Patent Office, Sales Branch, St Max7 Cray, Orpington, Kent BR5 3RD. Printed by Multiplex techniques ltd, St Mary Cray, Kent. Com 1/87.